Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J39/00—Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
  • B01J39/04—Processes using organic exchangers
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
  • A23F3/00—Tea; Tea substitutes; Preparations thereof
  • A23F3/16—Tea extraction; Tea extracts; Treating tea extract; Making instant tea
  • A23F3/18—Extraction of water soluble tea constituents
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
  • A23F3/00—Tea; Tea substitutes; Preparations thereof
  • A23F3/16—Tea extraction; Tea extracts; Treating tea extract; Making instant tea
  • A23F3/22—Drying or concentrating tea extract
  • A23F3/225—Drying or concentrating tea extract by evaporation, e.g. drying in thin layers, foam drying
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
  • A23F5/00—Coffee; Coffee substitutes; Preparations thereof
  • A23F5/24—Extraction of coffee; Coffee extracts; Making instant coffee
  • A23F5/26—Extraction of water-soluble constituents
  • A23F5/267—Extraction of water-soluble constituents using additives, specific extraction media or specific coffee blends
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
  • A23F5/00—Coffee; Coffee substitutes; Preparations thereof
  • A23F5/24—Extraction of coffee; Coffee extracts; Making instant coffee
  • A23F5/28—Drying or concentrating coffee extract
  • A23F5/285—Drying or concentrating coffee extract by evaporation, e.g. drying in thin layers, foam drying
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
  • A23F5/00—Coffee; Coffee substitutes; Preparations thereof
  • A23F5/46—Coffee flavour; Coffee oil; Flavouring of coffee or coffee extract
  • A23F5/48—Isolation or recuperation of coffee flavour or coffee oil
  • A23F5/50—Isolation or recuperation of coffee flavour or coffee oil from coffee extract
  • A23F5/505—Isolation or recuperation of coffee flavour or coffee oil from coffee extract by distillation, e.g. stripping the extract; Recovering volatile gases, e.g. during concentration
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
  • A23L5/00—Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
  • A23L5/20—Removal of unwanted matter, e.g. deodorisation or detoxification

Definitions

• the present invention is concerned with the treatment of aqueous media containing residual substances.
• aqueous waste liquids from the food industry contain substances that are liable to exert an undesirable effect on certain characteristics of the medium into which they are discharged, in particular on the oxygen content of the aqueous medium.
• aqueous effluents produced during the extraction of vegetable materials such as coffee, chicory or tea, in particular the liquids obtained by condensation of vapours emitted by aqueous extracts during concentration operations, which contain a variety of organic substances as well as certain mineral substances.
• the present invention is concerned with a particularly simple and effective process for purifying these aqueous effluents. It provides a process for purifying an aqueous liquid resulting from the condensation of vapours emitted by an aqueous extract of a vegetable material, in which the liquid is treated with at least one ion exchange resin.
• this purification treatment considerably reduces the concentration of oxidisable substances in the aqueous liquid.
• this concentration expressed by the C.O.D. (Chemical Oxygen Demand) of the medium, may be reduced from 2000 ppm to a value of the order of 100 to 500 ppm.
• the aqueous liquid obtained after treatment with the ion exchange resins may be either discharged as waste water or be utilised for the aqueous extraction of a fresh batch of vegetable material. This latter application is be particularly advantageous within in the production of extracts of vegetable materials such as coffee, chicory or tea.
• utilising the liquid treated by the process in accordance with the invention for the aqueous extraction of the vegetable material leads to an improvement in the aromatic characteristics of the resulting product.
• the purified aqueous liquid may also be used for feeding steam boilers. It is preferable, in this case, to submit the liquid to a further purification, for example by filtration on activated charcoal, before introducing it into the boiler.
• the operational parameters of the process may be selected having regard to the respective characteristics of the aqueous liquid to be purified and of the treated liquid. For example, it is possible to choose the parameters so as to obtain a purified liquid having a C.O.D. determined for example by the potassium dichromate test set out in the ASTM Standard No D 1252-58 T, not exceeding a given value, such as 300 ppm.
• Anionic or cationic ion exchange resins may be chosen from the resins industrially available.
• resins that are particularly suitable for carrying out the process in accordance with the invention are the anionic resins, known under the designation Dowex 11, 3 or 2 or cationic resins such as Dowex 50 resin.
• the appropriate quantity of resin expressed as a proportion of the quantity of aqueous liquid to be treated, may be readily determined as a function of the purity of the purified product that it is desired to obtain. This quantity may be expressed, for example, as the maximum useful life of a given quantity of resin for a given throughput of a particular aqueous product.
• the order of magnitude of this maximum useful life may also be calculated on the basis of the absorption capacity of the resin used.
• a first approximation shows that this volume of resin will absorb a most 156 kg of organic substance.
• This volume of resin will thus be able to treat 78 tons of aqueous product, which, for a throughput of 10 tons/hour of aqueous product, gives a maximum life of the resin of the order of 8 hours.
• the conditions of flow of the aqueous liquid through the ion exchange resin are not critical in relation to the process in accordance with the invention. These conditions are governed essentially by the geometry of the column containing the ion exchange resin as well as by the throughput of the treated product. In general, it is preferred to use cylindrical columns with a height of approximately 5 to 10 times the diameter, the velocity of the aqueous fluid through the resin being of the order of 0.7 cm/s to 1.0 cm/s.
• the temperature of the treatment is not critical with respect to the operation of the process, provided that it does not impair the absorption properties of the resins. In general, it is preferable to carry out the purification treatment at ambient temperature.
• the resin used may subsequently be regenerated for re-use.
• An anion exchange resin may be conveniently regenerated with an aqueous alkali solution, for example an aqueous sodium hydroxide solution.
• the appropriate quantity of alkaline solution may be calculated on the basis that the quantity of absorbed organic substances expressed, for example, in moles per liter of resin, is to be replaced by an equivalent molar quantity of alkaline substance (OH - ions).
• an anionic resin having reached its absorption capacity for example 1.2 moles per liter of resin
• 1.2 moles of sodium hydroxide per liter of resin should be used for complete regeneration.
• a cation exchange resin may be regenerated with an aqueous acid solution, for example an aqueous solution of hydrochloric acid.
• the appropriate quantity of acid solution may be determined by calculation on the basis that the molar quantity of absorbed organic substances is to be replaced by an equivalent molar quantity of acid (H + ions). For example, if an aqueous solution containing 35% by weight of hydrochloric acid is used, 1.3 m 3 of cation exchange resin which has absorbed its maximum of 1.2 moles per liter may be regenerated with 180 liters of solution, allowing for an approximately 20% excess.
• the regeneration of the ion exchange resin may be effected by contacting the resin with the alkaline or acid solution for a period of time, of the order of 1 hour or more, that is sufficient for the absorbed organic substances to be replaced by the appropriate OH - or H + ions.
• Regeneration is preferably carried out by passing the alkaline or acid solution through the resin at a rate such that the appropriate quantity of the regenerating liquid is used, for example a rate of 50 liters/hour of sodium hydroxide solution for 5 hours for 1.3 m 3 of the anionic resin considered above.
• the regenerating solution used preferably contains a concentration by weight of the alkaline or acid substance that does not exceed 30 to 35%.
• the resin is preferably washed with water, preferably with a volume of water corresponding approximately to 5 times the volume of the washed resin, and at a rate of flow approximately equal to the rate of flow of the aqueous liquid treated.
• the process in accordance with the invention may comprise successive treatments of the aqueous liquid, with similar or different types of resin.
• this treatment it is preferable to carry out this treatment by passage through columns arranged in series and containing different types of resins, i.e. of the anionic and cationic type.
• the process according to the invention is particularly suitable for the treatment of condensates resulting from concentration of aqueous coffee or chicory extracts.
• the aqueous extract is stripped and a portion of its aromatic constituents is recovered for subsequent addition to the extract after concentration.
• the evaporation condensate is collected and led to a purification installation comprising several batteries of columns filled with ion exchange resins.
• Each battery comprises two series-connected columns, with the first column containing an anionic resin and the second a cationic resin.
• Each battery may also comprise other cationic or anionic columns.
• the aqueous liquid is recycled to the extraction of the vegetable material.
• the aqueous liquid is led into another battery, and the saturated battery is regenerated and washed.
• the invention is illustrated by the following examples.
• the content of organic substances in the liquid is expressed as the C.O.D. determined by the potassium dichromate test set out in ASTM standard No D 1252-58 T. This test may be described schematically in the following manner:
• a sample of 50 ml of the aqueous medium is heated under reflux in the presence of 25 ml of a standard solution of potassium dichromate (0.250 N) and 75 ml concentrated sulphuric acid, and the excess potassium dichromate is titrated with ferrous ammonium sulphate.
• the quantity of oxidizable organic substances which is proportional to the quantity of potassium dichromate consumed, expressed in ppm, is the C.O.D. of the aqueous medium.
• a stripped aqueous coffee extract is concentrated by evaporation and the vapours are condensed.
• This condensate having a C.O.D. of 1320 ppm, is fed at the rate of 20 kg/h into a purifier battery comprising the following series-connected columns:
• the C.O.D. of the product may be further reduced by again repeating the ion exchange resin treatment.
• a condensate resulting from the concentration by evaporation of an aqueous extract of chicory, with a C.O.D. of 1400 ppm, is passed at the rate of 20 kg/h through a purification battery consisting of three series-connected columns having the following characteristics:
• Two samples, 1 and 2 are withdrawn every hour at the exit of the 2nd and 3rd columns and are examined by the dichromate test.
• the purified aqueous liquid obtained in Example 1 is recycled to the aqueous extraction of coffee. It is heated to a temperature of 180°C and added continuously to the water used for extraction in the proportion of 50% by volume.
• the purification battery is changed after operating for 8 hours, the resins used being given the following regeneration treatment:
• the aqueous extract obtained by extraction using purified condensate is concentrated and freeze-dried.
• reconstitutes beverages are prepared starting from an extract obtained as described in this Example, and from an extract obtained under identical conditions, but without recycling of the purified condensate.
• the beverages, reconstituted in the proportion of 17 g extract per liter of hot water, are submitted in a triangle test to a panel of 10 trained tasters. 8 tasters resolved the triangle, and assessed the flavour of the beverage obtained from the extract prepared with recycled condensate to be fuller than the control.

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• Chemical & Material Sciences (AREA)
• Life Sciences & Earth Sciences (AREA)
• Engineering & Computer Science (AREA)
• Food Science & Technology (AREA)
• Polymers & Plastics (AREA)
• Nutrition Science (AREA)
• Health & Medical Sciences (AREA)
• Organic Chemistry (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Oil, Petroleum & Natural Gas (AREA)
• Treatment Of Liquids With Adsorbents In General (AREA)
• Tea And Coffee (AREA)
• Extraction Or Liquid Replacement (AREA)
• Treatment Of Water By Ion Exchange (AREA)
• Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Applications Claiming Priority (2)

Publications (1)

Family

ID=4431191

Family Applications (1)

Country Status (9)

Cited By (3)

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Citations (6)

Family Cites Families (1)

• 1972
  • 1972-12-14 CH CH1819672A patent/CH559570A5/xx not_active IP Right Cessation
• 1973
  • 1973-12-04 ZA ZA739215A patent/ZA739215B/xx unknown
  • 1973-12-05 CA CA187,443A patent/CA1021190A/en not_active Expired
  • 1973-12-10 DE DE2361388A patent/DE2361388A1/de not_active Ceased
  • 1973-12-10 GB GB5718573A patent/GB1410308A/en not_active Expired
  • 1973-12-11 US US05/423,660 patent/US3972809A/en not_active Expired - Lifetime
  • 1973-12-12 FR FR7344410A patent/FR2220478B1/fr not_active Expired
  • 1973-12-13 ES ES421416A patent/ES421416A1/es not_active Expired
  • 1973-12-14 JP JP48140216A patent/JPS5076275A/ja active Pending

Patent Citations (6)

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